JP2020157191A - Air bubble separation/removal device - Google Patents

Air bubble separation/removal device Download PDF

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JP2020157191A
JP2020157191A JP2019057036A JP2019057036A JP2020157191A JP 2020157191 A JP2020157191 A JP 2020157191A JP 2019057036 A JP2019057036 A JP 2019057036A JP 2019057036 A JP2019057036 A JP 2019057036A JP 2020157191 A JP2020157191 A JP 2020157191A
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liquid
bubble
fluid chamber
bubbles
outlet
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土屋 一俊
Kazutoshi Tsuchiya
一俊 土屋
一男 三科
Kazuo Mishina
一男 三科
大輔 川杉
Daisuke Kawasugi
大輔 川杉
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TNK Corp Ltd
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TNK Corp Ltd
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Abstract

To provide an air bubble separation/removal device improved so as to be able to separate and remove only gas constituting air bubble included in fluid.SOLUTION: The air bubble separation/removal device is equipped with: an air bubble removal device 120 that separates liquid from which air bubble should be removed flowing in through an inflow port P1 into first liquid having air bubble removed and second liquid containing the air bubble, by utilizing swirl flow of the liquid from which the air bubble should be removed, makes the first liquid flow out through a first outflow port P1 and makes the second liquid flow out through a second outflow port P2; a sub tank 130, into which the second liquid flown out through the second outflow port P2 flows, which has a float valve 142 at an upper part thereof; a downstream adjustment valve 143 arranged at first air bubble removal fluid outflow piping 145 connected to the first outflow port P1; and a return adjustment valve 144 arranged in a second air bubble removal fluid outflow piping 146 whose one end is connected to a bottom part of the sub tank 130 and whose other end is connected to a downstream side of the downstream adjustment valve 143 of the first air bubble removal fluid outflow piping 145.SELECTED DRAWING: Figure 1

Description

この発明は、液体中に含まれる気泡を旋廻流を利用して分離除去する気泡分離除去装置に関し、詳しくは液体中から気泡を構成する気体のみを分離除去できるように改良した気泡分離除去装置に関する。 The present invention relates to a bubble separation / removal device that separates and removes bubbles contained in a liquid by using a rotating flow, and more particularly to an improved bubble separation / removal device that can separate and remove only the gas constituting the bubbles from the liquid. ..

液体中から気泡を除去する要求は各種分野において存在する。例えば、食品、薬品の製造過程において、原料となる液体中に気泡が混入してしまうと好ましくない場合があり、この場合は原料となる液体から効率よく気泡を分離除去する必要がある。 There are demands in various fields for removing air bubbles from a liquid. For example, in the manufacturing process of foods and chemicals, it may not be preferable if bubbles are mixed in the liquid as a raw material. In this case, it is necessary to efficiently separate and remove the bubbles from the liquid as a raw material.

従来、この種の気泡分離除去装置としては、特許文献1に開示されたものが知られている。 Conventionally, as this kind of bubble separation / removal device, the one disclosed in Patent Document 1 is known.

この特許文献1に開示された「液体中の気泡除去装置」においては、1端に少なくとも1個の流入口と他端に流出口とを有する流体室から構成され、前記流入口が液体に流体室の内壁に対して接線流れを生ぜしめる気泡除去装置において、前記流体室は前記流入口から流出口方向へ直径が漸次連続して減少する第1流体室と、該第1流体室に接続し、直径が他端方向へ漸次連続して増大する第2流体室とから形成されていることと、前記第1流体室の前記流入口側の端面から、前記第1流体室と前記第2流体室との接合位置付近までの間に開口する放気口、または前記位置までの間に開口する気体放気細管が、前記流体室の軸心に対して共軸に設けられて構成される。 The "bubble removing device in a liquid" disclosed in Patent Document 1 is composed of a fluid chamber having at least one inflow port at one end and an outflow port at the other end, and the inflow port is a fluid in a liquid. In the bubble removing device that creates a tangential flow with respect to the inner wall of the chamber, the fluid chamber is connected to a first fluid chamber whose diameter gradually and continuously decreases from the inlet to the outlet, and the first fluid chamber. The first fluid chamber and the second fluid are formed from the second fluid chamber whose diameter gradually and continuously increases toward the other end, and from the end surface of the first fluid chamber on the inflow port side. An air outlet that opens up to the vicinity of the joint position with the chamber or a gas air exhaust tube that opens up to the position is provided on the same axis with respect to the axial center of the fluid chamber.

特開平5−84403号公報Japanese Unexamined Patent Publication No. 5-84403

ところで、上記特許文献1に記載された「液体中の気泡除去装置」において、放気口又は気体放気細管からは気泡を構成する気体と若干の液体が排出されるが、この排出される若干の液体も気泡除去液体の中に取り込みたいという要望がある。 By the way, in the "air bubble removing device in liquid" described in Patent Document 1, gas constituting bubbles and some liquid are discharged from the air outlet or the gas air vent tube, but the discharged slightly There is a desire to incorporate this liquid into the bubble removal liquid.

そこで、この発明は、流体中に含まれる気泡を構成する気体のみを分離除去できるように改良した気泡分離除去装置を提供することを目的とする。 Therefore, an object of the present invention is to provide an improved bubble separation / removal device that can separate and remove only the gas constituting the bubbles contained in the fluid.

上記目的を達成するため、請求項1の発明は、流入口から流入した気泡除去対象液体を該気泡除去対象液体の旋回流を利用して気泡が除去された第1の液体と気泡を含む第2の液体とに分離し、前記第1の液体を第1の流出口から流出し、前記第2の液体を第2の流出口から流出する気泡分離装置と、前記第2の流出口から流出される第2の液体が流入し、上部にフロートバルブが設けられたサブタンクと、前記第1の流出口に接続された第1の気泡除去流体流出配管に配置される下流調整バルブと、一端が前記サブタンクの底部に接続され、他端が前記第1の気泡除去流体流出配管の前記下流調整バルブの下流側に接続された第2の気泡除去流体流出配管に配置される戻り調節バルブと、を具備することを特徴とする。 In order to achieve the above object, the invention of claim 1 includes a first liquid in which bubbles have been removed and bubbles in the liquid to be removed from bubbles flowing from the inflow port by utilizing a swirling flow of the liquid to be removed. A bubble separation device that separates into two liquids, discharges the first liquid from the first outlet, and discharges the second liquid from the second outlet, and flows out from the second outlet. A sub-tank provided with a float valve at the top, a downstream adjusting valve arranged in a first bubble removing fluid outflow pipe connected to the first outlet, and one end thereof. A return regulating valve connected to the bottom of the sub-tank and the other end of which is arranged in a second bubble removing fluid outflow valve connected to the downstream side of the downstream adjusting valve of the first bubble removing fluid outflow pipe. It is characterized by having.

請求項2の発明は、請求項1に記載の発明において、前記気泡分離装置は、前記サブタンク内に設けられ、前記第1の気泡除去流体流出配管は、前記サブタンクの底面を通って前記気泡分離装置の前記第1の流出口に接続されることを特徴とする。 The invention of claim 2 is the invention of claim 1, wherein the bubble separation device is provided in the sub tank, and the first bubble removing fluid outflow pipe passes through the bottom surface of the sub tank to separate the bubbles. It is characterized in that it is connected to the first outlet of the device.

請求項3の発明は、請求項1又は2に記載の発明において、前記気泡分離装置は、前記流入口から流入された前記気泡除去対象液体の旋回流を形成する旋回流形成部と、前記旋回流形成部で形成された旋回流の下流側に向かって漸次径が小となる第1の流体室と、前記第1の流体室の中心軸上に設けられ、一端が該第1の流体室内に開口する放気管と、前記第1の流体室の下流側に設けられた第2の流体室と、を具備し、前記第2の流体室に前記第1の流出口が設けられ、前記放気管に前記第2の流出口が設けられることを特徴とする。 The invention according to claim 3 is the invention according to claim 1 or 2, wherein the bubble separating device has a swirling flow forming portion for forming a swirling flow of the fluid to be removed from bubbles flowing in from the inflow port, and the swirling flow forming portion. A first fluid chamber whose diameter gradually decreases toward the downstream side of the swirling flow formed by the flow forming portion, and a first fluid chamber provided on the central axis of the first fluid chamber, one end of which is the first fluid chamber. A second fluid chamber provided on the downstream side of the first fluid chamber is provided, and the first outlet is provided in the second fluid chamber to provide the first outlet. The trachea is provided with the second outlet.

請求項4の発明は、請求項1又は2に記載の発明において、前記気泡分離装置は、前記流入口から流入された前記気泡除去対象液体の旋回流を形成する旋回流形成部と、前記旋回流形成部で形成された旋回流の下流側に向かって漸次径が小となる第1の流体室と、前記第1の流体室の中心軸上に設けられ、一端が該第1の流体室内に突出する放気管と、前記放気管の突出部周縁に形成され、前記旋回流の下流側に向かって漸次径が小さくなるテーパー壁と、前記第1の流体室の下流側に設けられた第2の流体室と、を具備し、前記第2の流体室に前記第1の流出口が設けられ、前記放気管に前記第2の流出口が設けられることを特徴とする。 The invention of claim 4 is the invention according to claim 1 or 2, wherein the bubble separating device has a swirling flow forming portion for forming a swirling flow of the fluid to be removed from bubbles flowing in from the inflow port, and the swirling flow forming portion. A first fluid chamber whose diameter gradually decreases toward the downstream side of the swirling flow formed by the flow forming portion, and a first fluid chamber provided on the central axis of the first fluid chamber, one end of which is the first fluid chamber. A tapered wall formed on the periphery of the protruding portion of the air vent tube and gradually decreasing in diameter toward the downstream side of the swirling flow, and a first provided on the downstream side of the first fluid chamber. It is characterized in that the second fluid chamber is provided with the first outlet, and the air outlet is provided with the second outlet.

この発明によれば、流入口から流入した気泡除去対象液体を該気泡除去対象液体の旋回流を利用して気泡が除去された第1の液体と気泡を含む第2の液体とに分離し、前記第1の液体を第1の流出口から流出し、前記第2の液体を第2の流出口から流出する気泡分離装置と、前記第2の流出口から流出される第2の液体が流入し、上部にフロートバルブが設けられたサブタンクと、前記第1の流出口に接続された第1の気泡除去流体流出配管に配置される下流調整バルブと、一端が前記サブタンクの底部に接続され、他端が前記第1の気泡除去流体流出配管の前記下流調整バルブの下流側に接続された第2の気泡除去流体流出配管に配置される戻り調節バルブと、を具備して構成したので、流体中に含まれる気泡を構成する気体のみを分離除去できるという効果を奏する。 According to the present invention, the bubble removal target liquid flowing in from the inflow port is separated into a first liquid from which bubbles have been removed and a second liquid containing bubbles by utilizing the swirling flow of the bubble removal target liquid. A bubble separator that allows the first liquid to flow out of the first outlet and the second liquid to flow out of the second outlet, and a second liquid that flows out of the second outlet flow in. A sub-tank provided with a float valve at the top, a downstream adjusting valve arranged in the first air bubble removing fluid outflow pipe connected to the first outlet, and one end connected to the bottom of the sub-tank. Since the other end is provided with a return adjusting valve arranged in the second bubble removing fluid outflow pipe connected to the downstream side of the downstream adjusting valve of the first bubble removing fluid outflow pipe, the fluid is provided. It has the effect of being able to separate and remove only the gas that constitutes the bubbles contained therein.

図1は、この発明に係わる気泡分離除去装置を用いて構成した気泡分離除去システムの一例を示す流体回路図である。FIG. 1 is a fluid circuit diagram showing an example of a bubble separation / removal system configured by using the bubble separation / removal device according to the present invention. 図2は、図1に示した流体回路図で使用する気泡分離除去装置の一例の概略断面図である。FIG. 2 is a schematic cross-sectional view of an example of the bubble separation / removal device used in the fluid circuit diagram shown in FIG. 図3は、図2に示した気泡分離装置の一例及び他の例を示す略図である。FIG. 3 is a schematic view showing an example and another example of the bubble separation device shown in FIG.

以下、この発明に係わる気泡分離除去装置の実施の形態を添付図面を参照して詳細に説明する。 Hereinafter, embodiments of the bubble separation / removal device according to the present invention will be described in detail with reference to the accompanying drawings.

図1は、この発明に係わる気泡分離除去装置を用いて構成した気泡分離除去システムの一例を示す流体回路図である。 FIG. 1 is a fluid circuit diagram showing an example of a bubble separation / removal system configured by using the bubble separation / removal device according to the present invention.

図1において、メインタンク110は、この気泡分離除去装置100で気泡が分離除去される気泡除去対象液体が収容される。メインタンク110に収納された気泡除去対象液体は、141で加圧されて、気泡分離装置120の流入口P0に流入する。 In FIG. 1, the main tank 110 contains a liquid to be removed by bubbles, from which bubbles are separated and removed by the bubble separation / removal device 100. The liquid to be removed from bubbles stored in the main tank 110 is pressurized by 141 and flows into the inflow port P0 of the bubble separator 120.

気泡分離除去装置100は、気泡分離装置120、サブタンク130、フロートバルブ142、下流調整バルブ143、戻り調節バルブ144を具備して構成される。 The bubble separation / removal device 100 includes a bubble separation device 120, a sub tank 130, a float valve 142, a downstream adjustment valve 143, and a return adjustment valve 144.

ここで、気泡分離装置120は、流入口P0から流入した気泡除去対象液体を該気泡除去対象液体の旋回流を利用して気泡が除去された第1の液体と気泡を含む第2の液体とに分離し、第1の液体を第1の流出口P1から流出し、第2の液体を第2の流出口P2から流出する。この気泡分離装置120の詳細は、後に図3を参照して説明する。 Here, the bubble separation device 120 uses the swirling flow of the bubble removal target liquid as the bubble removal target liquid that has flowed in from the inflow port P0 to form a first liquid from which bubbles have been removed and a second liquid containing bubbles. The first liquid flows out from the first outlet P1 and the second liquid flows out from the second outlet P2. Details of the bubble separator 120 will be described later with reference to FIG.

気泡分離装置120の第2の流出口P2から流出した気泡を含む第2の液体は、サブタンク130に導かれる。サブタンク130は、上部にフロートバルブ142が設けられており、気泡分離装置120の第2の流出口P2から流入した気泡を含む第2の液体から気泡を集め、この気泡を集めた気体をフロートバルブ142を介して外部に放気する。なお、サブタンク130の内部には、気泡の除去性能を上げるためのバッフルプレート131を設けてもよい。 The second liquid containing the bubbles flowing out from the second outlet P2 of the bubble separator 120 is guided to the sub tank 130. The sub tank 130 is provided with a float valve 142 at the upper part, collects bubbles from a second liquid containing bubbles flowing in from the second outlet P2 of the bubble separator 120, and uses the collected gas as the float valve. It is released to the outside through 142. A baffle plate 131 may be provided inside the sub tank 130 to improve the bubble removing performance.

気泡分離装置120の第1の流出口P1から流出する気泡が除去された第1の液体は、第1の流出口P1の流出口P1に接続された第1の気泡除去流体流出配管145に流れ、この第1の気泡除去流体流出配管145には下流調整バルブ143が設けられている。 The first liquid from which the bubbles flowing out from the first outlet P1 of the bubble separator 120 have been removed flows to the first bubble removing fluid outflow pipe 145 connected to the outlet P1 of the first outlet P1. A downstream adjusting valve 143 is provided in the first bubble removing fluid outflow pipe 145.

サブタンク130の底部には、サブタンク130で気泡が分離された液体が流れる第2の気泡除去流体流出配管146が接続され、この第2の気泡除去流体流出配管146には、戻り調節バルブ144が設けられている。 A second bubble removing fluid outflow pipe 146 through which the liquid separated by the bubbles flows flows is connected to the bottom of the sub tank 130, and a return adjusting valve 144 is provided in the second bubble removing fluid outflow pipe 146. Has been done.

下流調整バルブ143を通過した気泡が除去された液体及び戻り調節バルブ144を通過した気泡が除去された液体は気泡除去流体排出配管147に合流して排出される。 The liquid from which the air bubbles that have passed through the downstream adjustment valve 143 and the liquid from which the air bubbles that have passed through the return adjustment valve 144 have been removed merge with the bubble removal fluid discharge pipe 147 and are discharged.

上記気泡分離除去装置100の動作を説明すると以下のようになる。 The operation of the bubble separation / removal device 100 will be described as follows.

1)気泡分離装置120は、流入口P0から気泡除去対象液体を流入し、該気泡除去対象液体の旋回流を利用して気泡が除去された第1の液体と気泡を含む第2の液体とに分離する。 1) The bubble separation device 120 flows in the liquid to be removed from bubbles from the inflow port P0, and uses the swirling flow of the liquid to be removed to remove bubbles to remove bubbles from the first liquid and the second liquid containing bubbles. Separate into.

2)気泡分離装置120で分離された第1の液体は第1の流出口P1から第1の気泡除去流体流出配管145、下流調整バルブ143を通って気泡除去流体排出配管147から排出される。 2) The first liquid separated by the bubble separating device 120 is discharged from the bubble removing fluid discharge pipe 147 from the first outlet P1 through the first bubble removing fluid outflow pipe 145 and the downstream adjusting valve 143.

3)気泡分離装置120で分離された第2の液体は第2の流出口P2からサブタンク130に導かれる。 3) The second liquid separated by the bubble separating device 120 is guided from the second outlet P2 to the sub tank 130.

4)そして、サブタンク130内が気泡が分離された液体で満たされるまでフロートバルブ142は開になっていて、サブタンク130内で集められた気体はフロートバルブ142を通って外部に放気される。 4) Then, the float valve 142 is open until the inside of the sub tank 130 is filled with the liquid in which bubbles are separated, and the gas collected in the sub tank 130 is released to the outside through the float valve 142.

5)しばらくすると、サブタンク130内が気泡が分離された液体で満たされフロートバルブ142のフロートは上昇してフロートバルブ142は閉じられる。この状態でサブタンク130内の気泡が分離された液体は、第2の気泡除去流体流出配管146、戻り調節バルブ144を通り、気泡除去流体排出配管147から排出される。 5) After a while, the inside of the sub tank 130 is filled with the liquid from which bubbles are separated, the float of the float valve 142 rises, and the float valve 142 is closed. In this state, the liquid in which the bubbles are separated in the sub tank 130 passes through the second bubble removing fluid outflow pipe 146 and the return adjustment valve 144, and is discharged from the bubble removing fluid discharge pipe 147.

気泡分離除去装置100は運転状態において、上記4)と5)の動作を繰り返し、気泡除去対象液体から分離除去した気体のみを大気放出する。 The bubble separation / removal device 100 repeats the operations 4) and 5) above in the operating state, and releases only the gas separated and removed from the liquid to be removed from the bubbles into the atmosphere.

ここで、下流調整バルブ143は、この気泡分離除去装置100の気泡除去具合を調整し、戻り調節バルブ144は、サブタンク130内の液面保持圧力の調整を行う。 Here, the downstream adjustment valve 143 adjusts the bubble removal condition of the bubble separation / removal device 100, and the return adjustment valve 144 adjusts the liquid level holding pressure in the sub tank 130.

図2は、図1に示した流体回路図で使用する気泡分離除去装置の一例の概略断面図である。この図2に示す気泡分離除去装置100は、サブタンク130内に気泡分離装置120を収容して構成される。この構成において、第1の気泡除去流体流出配管145は、サブタンク130の底面を通って気泡分離装置100の第1の流出口P1に接続される。また、気泡分離装置100の第2の流出口P2は、サブタンク130に設けられ、第2の液体をサブタンク130内に直接流出させる。その他の構成は図1に示した気泡分離除去装置100と同様である。 FIG. 2 is a schematic cross-sectional view of an example of the bubble separation / removal device used in the fluid circuit diagram shown in FIG. The bubble separation / removal device 100 shown in FIG. 2 is configured by accommodating the bubble separation device 120 in the sub tank 130. In this configuration, the first bubble removing fluid outflow pipe 145 is connected to the first outlet P1 of the bubble separator 100 through the bottom surface of the sub tank 130. Further, the second outlet P2 of the bubble separation device 100 is provided in the sub tank 130, and the second liquid is directly discharged into the sub tank 130. Other configurations are the same as those of the bubble separation / removal device 100 shown in FIG.

図3は、図1及び図2に示した気泡分離装置120の一例(図3(A))及び他の例(図3(B))を示す略図である。 FIG. 3 is a schematic view showing an example (FIG. 3 (A)) and another example (FIG. 3 (B)) of the bubble separator 120 shown in FIGS. 1 and 2.

図3において、この発明に係わる気泡分離除去装置100の気泡分離装置120詳細の一例は図3(A)に示される。図3(A)に示される気泡分離装置120は、図1及び図2に示す流入口P0から流入された気泡除去対象液体から気泡除去対象液体の旋回流を形成する旋回流形成部122と、第1の流体室123と、第1の流体室123の下流側に設けられた第2の流体室124と、第1の流体室123内に一端が開口している放気管125とを具備している。 In FIG. 3, an example of details of the bubble separation device 120 of the bubble separation / removal device 100 according to the present invention is shown in FIG. 3 (A). The bubble separation device 120 shown in FIG. 3A includes a swirl flow forming unit 122 that forms a swirl flow of the bubble removal target liquid from the bubble removal target liquid flowing in from the inflow port P0 shown in FIGS. 1 and 2. It includes a first fluid chamber 123, a second fluid chamber 124 provided on the downstream side of the first fluid chamber 123, and an air discharge pipe 125 having one end open in the first fluid chamber 123. ing.

ここで、旋回流形成部122は、この旋回流形成部122の外周に沿って形成された環流路121と、この環流路121に接続される2か所に設けた図示しない吐出口を具備して構成される。 Here, the swirl flow forming portion 122 includes a ring flow path 121 formed along the outer circumference of the swirl flow forming portion 122, and discharge ports (not shown) provided at two locations connected to the ring flow path 121. It is composed of.

第1の流体室123は、下流側に向かって漸次径が小となる円錐台形状の内周壁123aに囲まれた空間からなり、旋回流形成部122で形成された気泡除去対象液体P0は、この内周壁123aに囲まれた空間内に流される。 The first fluid chamber 123 is composed of a space surrounded by a truncated cone-shaped inner peripheral wall 123a whose diameter gradually decreases toward the downstream side, and the liquid P0 for bubble removal formed by the swirling flow forming portion 122 is a liquid P0 to be removed. It is flushed into the space surrounded by the inner peripheral wall 123a.

第2の流体室124は、円筒形状からなり、一端は、第1の流体室123の下流側に接続され、他端は、この気泡分離除装置100で気泡が除去された第1の液体を流出する流出口P1を形成している。 The second fluid chamber 124 has a cylindrical shape, one end of which is connected to the downstream side of the first fluid chamber 123, and the other end of which is a first liquid from which bubbles have been removed by the bubble separation / removal device 100. It forms an outflow outlet P1.

放気管125は、第1の流体室123の中心軸上に設けられ、一端に、第1の流体室123内に突出して開口する開口部が設けられ、他端は、この気泡分離装置100で分離した気泡を含む第2の液体を排出する流出口P2を形成している。 The air exhaust pipe 125 is provided on the central axis of the first fluid chamber 123, one end of which is provided with an opening protruding into the first fluid chamber 123, and the other end of which is the bubble separator 100. It forms an outlet P2 that discharges a second liquid containing separated bubbles.

すなわち、流入口P1から流入された気泡除去対象液体は、旋回流形成部122の環流路121内を流れ、環流路121に接続された吐出口第1の流体室123の周壁の接線方向に沿って気泡除去対象液体P0を第1の流体室123内に吐出し、第1の流体室123内に気泡除去対象液体P0の旋回流を形成する。 That is, the liquid to be removed from bubbles flowing from the inflow port P1 flows in the ring flow path 121 of the swirl flow forming portion 122, and is along the tangential direction of the peripheral wall of the discharge port first fluid chamber 123 connected to the ring flow path 121. The liquid P0 to be removed from bubbles is discharged into the first fluid chamber 123, and a swirling flow of the liquid P0 to be removed from bubbles is formed in the first fluid chamber 123.

第1の流体室123内に形成された気泡除去対象液体P0の旋回流は、第1の流体室123の下流側に向かって漸次径が小となる円錐台形状の内周壁123aに囲まれた空間内を流れる。 The swirling flow of the liquid P0 to be removed from bubbles formed in the first fluid chamber 123 is surrounded by a truncated cone-shaped inner peripheral wall 123a whose diameter gradually decreases toward the downstream side of the first fluid chamber 123. It flows in the space.

ここで、気泡除去対象液体の旋廻流の遠心力により、気泡を含まない流体は第1の流体室123の周壁123a側へ、気泡は、図3(A)に気泡Bで示すように、第1の流体室123内の放気管125の開口部周辺に集められる。 Here, due to the centrifugal force of the swirling flow of the liquid to be removed from bubbles, the fluid containing no bubbles moves toward the peripheral wall 123a side of the first fluid chamber 123, and the bubbles move to the peripheral wall 123a side of the first fluid chamber 123, and the bubbles are shown by bubbles B in FIG. It is collected around the opening of the air outlet tube 125 in the fluid chamber 123 of 1.

そして、第1の流体室123内の放気管125の開口部周辺に集められた気泡Bは、第2の流体室124側から加わる背圧により放気管125内に引き込まれ、この気泡Bを含む第2の液体は放気管125の他端の流出口P2から排出される。 Then, the bubbles B collected around the opening of the air release tube 125 in the first fluid chamber 123 are drawn into the air release tube 125 by the back pressure applied from the second fluid chamber 124 side, and include the bubbles B. The second liquid is discharged from the outlet P2 at the other end of the air discharge pipe 125.

一方、放気管125により第1の流体室123内で気泡が除去された第2の液体は、第2の流体室124を通って、流出口P1から流出される。 On the other hand, the second liquid from which bubbles have been removed in the first fluid chamber 123 by the air vent pipe 125 passes through the second fluid chamber 124 and flows out from the outlet P1.

図3(B)は、図3(A)に示した気泡分離装置120の他の例を示す略図である。図3(B)に示す気泡分離装置120においては、図3(A)の気泡分離装置120の放気管125の突出部周縁にテーパー壁126が形成されており、第1の流体室123内に形成された気泡除去対象液体の旋回流は、第1の流体室123の下流側に向かって漸次径が小となる円錐台形状の内周壁123aと放気管125の突出部周縁に形成された下流側に向かって漸次径が小さくなるテーパー壁126とにより囲まれた空間内を流れる。 FIG. 3B is a schematic diagram showing another example of the bubble separator 120 shown in FIG. 3A. In the bubble separator 120 shown in FIG. 3 (B), a tapered wall 126 is formed on the peripheral edge of the protruding portion of the air release pipe 125 of the bubble separator 120 of FIG. 3 (A), and is formed in the first fluid chamber 123. The swirling flow of the liquid to be removed from bubbles is formed on the truncated cone-shaped inner peripheral wall 123a whose diameter gradually decreases toward the downstream side of the first fluid chamber 123 and the downstream formed on the peripheral edge of the protrusion of the air release pipe 125. It flows in a space surrounded by a tapered wall 126 whose diameter gradually decreases toward the side.

このテーパー壁126の存在により、テーパー壁126がない図3(A)場合に比較して、気泡Bを更に効率よく放気管125の開口部周辺に集めることが可能になるので、気泡除去率を高くすることができり、かつ圧力損失を小さくすることができる。 The presence of the tapered wall 126 makes it possible to collect the bubbles B more efficiently around the opening of the air discharge tube 125 as compared with the case of FIG. 3A without the tapered wall 126, so that the bubble removal rate can be increased. It can be increased and the pressure loss can be reduced.

これは、テーパー壁126により、旋回流形成部122により形成された気泡除去対象液体の旋廻流が流れる無駄な空間がなくなるので、第1の流体室123における気泡除去対象液体の乱流が大幅に減少し、また、気泡除去対象液体の流速の減衰量が小さくなるためであると考えられる。その他の構成は、図3(A)に示した気泡分離装置120と同様である。 This is because the tapered wall 126 eliminates the wasted space through which the swirling flow of the liquid to be removed from bubbles formed by the swirling flow forming portion 122 flows, so that the turbulent flow of the liquid to be removed from bubbles in the first fluid chamber 123 is significantly increased. It is considered that this is because the amount of decrease in the flow velocity of the liquid to be removed from bubbles is reduced. Other configurations are the same as those of the bubble separator 120 shown in FIG. 3 (A).

以上がこの発明の代表的な実施形態の一例であるが、本発明は、上記実施例及び図面に示す実施例に限定することなく、その要旨を変更しない範囲内で適宜変形して実施できるものである。 The above is an example of a typical embodiment of the present invention, but the present invention is not limited to the above-mentioned Examples and the Examples shown in the drawings, and can be appropriately modified and implemented without changing the gist thereof. Is.

100 気泡分離除去装置
110 メインタンク
120 気泡分離装置
122 旋回流形成部
123 第1の流体室
124 第2の流体室
125 放気管
126 テーパー壁
130 サブタンク
131 バッフルプレート
141 供給ポンプ
142 フロートバルブ
143 下流調整バルブ
144 戻り調節バルブ
145 第1の気泡除去流体流出配管
146 第2の気泡除去流体流出配管
147 気泡除去流体排出配管
P0 流入口
P1 第1の流出口
P2 第2の流出口
100 Bubble separation and removal device 110 Main tank 120 Bubble separation device 122 Swirling flow forming part 123 First fluid chamber 124 Second fluid chamber 125 Air discharge pipe 126 Tapered wall 130 Sub tank 131 Baffle plate 141 Supply pump 142 Float valve 143 Downstream adjustment valve 144 Return adjustment valve 145 First bubble removal fluid outflow pipe 146 Second bubble removal fluid outflow pipe 147 Bubble removal fluid discharge pipe P0 Inflow port P1 First outflow port P2 Second outflow port

Claims (4)

流入口から流入した気泡除去対象液体を該気泡除去対象液体の旋回流を利用して気泡が除去された第1の液体と気泡を含む第2の液体とに分離し、前記第1の液体を第1の流出口から流出し、前記第2の液体を第2の流出口から流出する気泡分離装置と、
前記第2の流出口から流出される第2の液体が流入し、上部にフロートバルブが設けられたサブタンクと、
前記第1の流出口に接続された第1の気泡除去流体流出配管に配置される下流調整バルブと、
一端が前記サブタンクの底部に接続され、他端が前記第1の気泡除去流体流出配管の前記下流調整バルブの下流側に接続された第2の気泡除去流体流出配管に配置される戻り調節バルブと、
を具備することを特徴とする気泡分離除去装置。
The liquid to be removed from bubbles that has flowed in from the inflow port is separated into a first liquid from which bubbles have been removed and a second liquid containing bubbles by using the swirling flow of the liquid to be removed from bubbles, and the first liquid is separated. A bubble separator that flows out from the first outlet and discharges the second liquid from the second outlet,
A sub-tank in which the second liquid flowing out from the second outlet flows in and a float valve is provided at the upper part, and
A downstream adjusting valve arranged in the first bubble removing fluid outflow pipe connected to the first outlet, and
A return regulating valve arranged at one end connected to the bottom of the sub-tank and the other end connected to a second bubble removing fluid outflow pipe connected to the downstream side of the downstream adjusting valve of the first bubble removing fluid outflow pipe. ,
A bubble separation / removal device, which comprises.
前記気泡分離装置は、前記サブタンク内に設けられ、
前記第1の気泡除去流体流出配管は、前記サブタンクの底面を通って前記気泡分離装置の前記第1の流出口に接続される
ことを特徴とする請求項1記載の気泡分離除去装置。
The bubble separating device is provided in the sub tank and is provided in the sub tank.
The bubble separation / removal device according to claim 1, wherein the first bubble removal fluid outflow pipe is connected to the first outlet of the bubble separation device through the bottom surface of the sub tank.
前記気泡分離装置は、
前記流入口から流入された前記気泡除去対象液体の旋回流を形成する旋回流形成部と、前記旋回流形成部で形成された旋回流の下流側に向かって漸次径が小となる第1の流体室と、
前記第1の流体室の中心軸上に設けられ、一端が該第1の流体室内に開口する放気管と、
前記第1の流体室の下流側に設けられた第2の流体室と、
を具備し、
前記第2の流体室に前記第1の流出口が設けられ、前記放気管に前記第2の流出口が設けられる
ことを特徴とする請求項1又は2に記載の気泡分離除去装置。
The bubble separator
A first swirling flow forming portion that forms a swirling flow of the liquid to be removed from bubbles that has flowed in from the inflow port, and a first that gradually decreases in diameter toward the downstream side of the swirling flow formed by the swirling flow forming portion. With the fluid chamber
An air vent tube provided on the central axis of the first fluid chamber and one end of which opens into the first fluid chamber.
A second fluid chamber provided on the downstream side of the first fluid chamber, and
Equipped with
The bubble separation / removal device according to claim 1 or 2, wherein the first outlet is provided in the second fluid chamber, and the second outlet is provided in the air exhaust pipe.
前記気泡分離装置は、
前記流入口から流入された前記気泡除去対象液体の旋回流を形成する旋回流形成部と、前記旋回流形成部で形成された旋回流の下流側に向かって漸次径が小となる第1の流体室と、
前記第1の流体室の中心軸上に設けられ、一端が該第1の流体室内に突出する放気管と、
前記放気管の突出部周縁に形成され、前記旋回流の下流側に向かって漸次径が小さくなるテーパー壁と、
前記第1の流体室の下流側に設けられた第2の流体室と、
を具備し、
前記第2の流体室に前記第1の流出口が設けられ、前記放気管に前記第2の流出口が設けられる
ことを特徴とする請求項1又は2に記載の気泡分離除去装置。
The bubble separator
A first swirling flow forming portion that forms a swirling flow of the liquid to be removed from bubbles that has flowed in from the inflow port, and a first that gradually decreases in diameter toward the downstream side of the swirling flow formed by the swirling flow forming portion. With the fluid chamber
An air vent tube provided on the central axis of the first fluid chamber and one end of which projects into the first fluid chamber.
A tapered wall formed on the periphery of the protruding portion of the air exhaust pipe and whose diameter gradually decreases toward the downstream side of the swirling flow.
A second fluid chamber provided on the downstream side of the first fluid chamber, and
Equipped with
The bubble separation / removal device according to claim 1 or 2, wherein the first outlet is provided in the second fluid chamber, and the second outlet is provided in the air exhaust pipe.
JP2019057036A 2019-03-25 2019-03-25 Air bubble separation/removal device Pending JP2020157191A (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2020157191A true JP2020157191A (en) 2020-10-01

Family

ID=72640852

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112897619A (en) * 2021-02-24 2021-06-04 山东友信暖通集团有限公司 Associated gas separation equipment for geothermal water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112897619A (en) * 2021-02-24 2021-06-04 山东友信暖通集团有限公司 Associated gas separation equipment for geothermal water
CN112897619B (en) * 2021-02-24 2024-02-20 山东友信节能科技有限公司 Geothermal water associated gas separation equipment

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